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JP2801682B2 - Collection device for seamless capsules or edible grains - Google Patents

Collection device for seamless capsules or edible grains

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Publication number
JP2801682B2
JP2801682B2 JP1254623A JP25462389A JP2801682B2 JP 2801682 B2 JP2801682 B2 JP 2801682B2 JP 1254623 A JP1254623 A JP 1254623A JP 25462389 A JP25462389 A JP 25462389A JP 2801682 B2 JP2801682 B2 JP 2801682B2
Authority
JP
Japan
Prior art keywords
medium liquid
tank
sedimentation tank
sedimentation
edible
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP1254623A
Other languages
Japanese (ja)
Other versions
JPH03114529A (en
Inventor
一起 小俣
章二 浅見
一雄 林
富也 細井
賢一 生田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Taisho Pharmaceutical Co Ltd
Original Assignee
Taisho Pharmaceutical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
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Priority to JP1254623A priority Critical patent/JP2801682B2/en
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  • General Preparation And Processing Of Foods (AREA)
  • Formation And Processing Of Food Products (AREA)
  • Manufacturing Of Micro-Capsules (AREA)

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は、シームレスカプセ又は可食粒の製造装置に
おいて、シームレスカプセル又は可食粒を回収するため
の装置に関するものである。
Description: TECHNICAL FIELD The present invention relates to an apparatus for collecting seamless capsules or edible grains in an apparatus for producing seamless capsules or edible grains.

「従来の技術」 第4図を参照して、シームレスカプセルの製造装置及
び従来の回収装置を説明する。
"Prior Art" A seamless capsule manufacturing apparatus and a conventional recovery apparatus will be described with reference to FIG.

1はゼラチン等の水溶液よりなる流動性及び粘性を有
する皮膜形成物質aのタンク、2は流動性及び粘性を有
する充填物質bのタンクで、各タンク1,2はそれぞれ図
示しない加熱用ジャケットを備えて内部の皮膜形成物質
a,充填物質bを加熱するように構成され、タンク1,2内
部の皮膜形成物質a,充填物質bは常時ほぼ定量に保たれ
るべく随時他より補給されるようになっている。
Reference numeral 1 denotes a tank of a fluid and viscous film-forming substance a made of an aqueous solution of gelatin or the like, 2 denotes a tank of a fluid and viscous filling substance b, and each of the tanks 1 and 2 has a heating jacket (not shown). Film forming substance inside
a, the filling substance b is heated, and the film-forming substance a and the filling substance b inside the tanks 1 and 2 are replenished as needed from time to time so as to be kept almost constant.

タンク1内の皮膜形成物質aは50〜65℃に加熱され、
加圧管11からの圧力により、給送パイプ12を経て複合ノ
ズル3の先端を大径な吐出ノズル31に送られる。
The film-forming substance a in the tank 1 is heated to 50 to 65 ° C.
The tip of the composite nozzle 3 is sent to the large-diameter discharge nozzle 31 through the feed pipe 12 by the pressure from the pressurizing pipe 11.

この例の装置において、皮膜形成物質aは、給送パイ
プ12の途中に設けられた中間の加熱タンク13により、さ
らに70〜80℃程度に加熱されてノズル31へ供給されるよ
うに構成されている。また、加圧管11を使用しない場合
は、給送パイプ12におけるバイパスパイプ14の定量ポン
プ15によって皮膜形成物質aを前述の経路で給送する。
In the apparatus of this example, the film forming substance a is configured to be further heated to about 70 to 80 ° C. by the intermediate heating tank 13 provided in the middle of the feeding pipe 12 and supplied to the nozzle 31. I have. When the pressurizing pipe 11 is not used, the film forming substance a is fed by the metering pump 15 of the bypass pipe 14 in the feeding pipe 12 through the above-described path.

充填物質bはタンク2内で50℃前後に加熱され、給送
パイプ21の途中に設けられた定量ポンプ22により、前記
給送パイプ21を経て複合ノズル3における吐出ノズル31
の内側の小径な吐出ノズル32へ送られる。
The filling substance b is heated to about 50 ° C. in the tank 2, and is discharged from the discharge nozzle 31 in the composite nozzle 3 through the feed pipe 21 by the metering pump 22 provided in the middle of the feed pipe 21.
Is sent to the small-diameter discharge nozzle 32 inside.

23は定量ポンプ22による充填物質bの微小な脈流を防
止し、前記小径な吐出ノズル32における内圧を一定に保
つアキュムレーター、24は充填物質bのレリーフ量調整
バルブである。
Reference numeral 23 denotes an accumulator for preventing a minute pulsating flow of the filling substance b by the metering pump 22 to keep the internal pressure of the small-diameter discharge nozzle 32 constant, and reference numeral 24 denotes a relief amount adjusting valve for the filling substance b.

大径の吐出ノズル31と小径の吐出ノズル32からなる複
合ノズル3は、下方に設けられているカプセル形成槽4
内の媒体液cの流れに沿い、下向きに臨ませてある。
A composite nozzle 3 composed of a large-diameter discharge nozzle 31 and a small-diameter discharge nozzle 32 is provided with a capsule forming tank 4 provided below.
It faces downward along the flow of the medium liquid c.

媒体液cは前記皮膜形成物質cとは非溶解な流動パラ
フィンからなり、回収タンク5内にある媒体液Cの一部
は、ポンプ52により配管51の途中に設けられた熱交換器
53に送られて5℃前後に冷却され、分岐配管54を経てカ
プセル形成槽4に送られる。
The medium liquid c is made of liquid paraffin insoluble in the film-forming substance c, and a part of the medium liquid C in the recovery tank 5 is provided by a pump 52 provided in the middle of a pipe 51 by a heat exchanger.
It is sent to 53 and cooled to about 5 ° C., and then sent to the capsule forming tank 4 via the branch pipe 54.

回収タンク5内にある媒体液cの他の一部は、他のポ
ンプ55により他の配管56の途中にある脈流発生器57で所
定周期の脈流となり、この脈流は、カプセル形成槽4内
の上部において、複合ノズル3の真下を囲むように設け
られた脈流ノズル6より吹き出される。
Another part of the medium liquid c in the recovery tank 5 is changed into a pulsating flow of a predetermined cycle by a pulsating flow generator 57 in the middle of another pipe 56 by another pump 55, and this pulsating flow is formed in a capsule forming tank. In the upper part in 4, the air is blown out from a pulsating nozzle 6 provided so as to surround immediately below the composite nozzle 3.

複合ノズル3からは、大径の吐出ノズル31から吐出さ
れる流動性を有する皮膜形成物質aの流れの中に、小径
な吐出ノズル32から吐出される流動性を有する充填物質
bの連続した流れを含むジェット流dが、前記媒体液c
の流れに沿って連続的に形成され、このジェット流d
は、前記脈流発生器57で発生した脈流のエネルギーによ
り、その流れ方向先端より前記脈流の周期と一致する間
隔で順次切断される。
From the composite nozzle 3, a continuous flow of the flowable filling substance b discharged from the small-diameter discharge nozzle 32 is included in the flow of the flowable film-forming substance a discharged from the large-diameter discharge nozzle 31. Jet stream d containing
The jet stream d is formed continuously along the flow of
Are sequentially cut from the leading end in the flow direction at intervals matching the cycle of the pulsating flow by the energy of the pulsating flow generated by the pulsating flow generator 57.

切断された各粒は、カプセル形成槽4の底部から内部
に突入した状態の補助筒41内を流下する媒体液cの液流
に沿って流れながら、皮膜形成物質aと充填物質bとの
表面張力により、皮膜形成物質aの中に充填物質bが包
まれた状態のシームレスカプセルeに順次形成された、
媒体液cの液流中で冷却凝固しながら、補助筒41の下端
部と連通した回収管70を経て媒体液cとともに回収装置
7へ順次送られる。
Each cut particle flows along the liquid flow of the medium liquid c flowing down in the auxiliary cylinder 41 in a state of protruding into the inside from the bottom of the capsule forming tank 4, and the surface of the film forming substance a and the filling substance b By the tension, a seamless capsule e in which the filler substance b was wrapped in the film-forming substance a was sequentially formed.
While being cooled and solidified in the flow of the medium liquid c, the medium liquid c is sequentially sent to the recovery device 7 together with the medium liquid c via the recovery pipe 70 communicating with the lower end of the auxiliary cylinder 41.

回収装置7は、側方へ排出口73を設けた回収槽71、及
び、この回収槽71内において、前記排出口73から一部が
外部に突出する状態に傾斜して設けられた網(金網)72
から構成され、網72で媒体液cから分離されたシームレ
スカプセルeは、回収槽71の側方に設けた図示しないコ
ンベヤ等により次の乾燥工程に送られるように構成され
ている。
The recovery device 7 includes a recovery tank 71 provided with a discharge port 73 on the side, and a net (wire mesh) provided in the recovery tank 71 with a part inclined from the discharge port 73 to the outside. ) 72
The seamless capsule e separated from the medium liquid c by the net 72 is sent to the next drying step by a not-shown conveyor or the like provided on the side of the recovery tank 71.

シームレスカプセルeと分離された媒体液cは、図示
しないろ過器を経て媒体液の回収タンク5へ回収され循
環する。
The medium liquid c separated from the seamless capsule e is recovered and circulated to the medium liquid recovery tank 5 through a filter (not shown).

シームレスカプセルeの製造に代えて可食粒を製造す
るときは、他の部分を前述と同様に運転しながら、定量
ポンプ22運転を止めて小径な吐出ノズル32を塞ぎ、ノズ
ル31のみから可食性の物質aを吐出させてジェット流を
形成する。これにより、前記シームレスカプセルとほぼ
同様な形状の可食粒が連続的に形成される。
When producing edible grains instead of producing the seamless capsule e, while operating the other parts in the same manner as described above, the operation of the metering pump 22 is stopped, the small-diameter discharge nozzle 32 is closed, and the edible Is ejected to form a jet stream. As a result, edible grains having substantially the same shape as the seamless capsule are continuously formed.

「発明が解決しようとする課題」 従来の回収装置7は、前記のようにシームレスカプセ
ル又は可食粒を網72に向けて媒体液とともに落下させる
ように構成されているので、カプセル又は可食粒の凝固
が充分ではない状態のとき、あるいは、例えば1000粒/
分以上のように高速で造粒する場合には、網72との衝突
によってカプセル又は可食粒が傷付き易い。
[Problem to be Solved by the Invention] Since the conventional recovery device 7 is configured to drop the seamless capsule or the edible particles together with the medium liquid toward the net 72 as described above, the capsule or the edible particles When the coagulation is not enough, or for example, 1000 grains /
When granulation is performed at a high speed such as a minute or more, capsules or edible grains are easily damaged by collision with the net 72.

また、特に微小な(例えば1.5mm以下の径)カプセル
や可食粒を製造する場合には、しばしば網72に目詰まり
を生じて媒体液との分離が不充分になり、さらに、微小
なメッシュの網を使用するのも媒体液との分離を阻害す
る。
In addition, particularly when producing minute capsules (eg, 1.5 mm or less in diameter) and edible grains, the mesh 72 is often clogged, resulting in insufficient separation from the medium liquid. The use of a net also hinders separation from the medium liquid.

本発明の目的は、前述のような欠点を改善した回収装
置を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a recovery device in which the above-mentioned disadvantages are improved.

「課題を解決するための手段」 本発明に係る回収装置は前述の目的を達成するため、
流動性及び粘性を有する物質の流れからなるジェット流
を、当該ジェット流を構成する物質とは非溶解な媒体液
の液流中で連続的に形成し、当該ジェット流を流れ方向
先端より順次所定長さに切断し、切断したものを前記媒
体液の液流中で順次所定形状のシームレスカプセル又は
可食粒に形成し、このシームレスカプセル又は可食粒を
前記媒体液とともに回収管を経て回収すべく構成した製
造装置において、前記回収管から媒体液が流入する状態
に沈殿槽を設けたものである。
"Means for solving the problem" The recovery device according to the present invention achieves the above-mentioned object,
A jet stream composed of a flow of a substance having fluidity and viscosity is continuously formed in a liquid stream of a medium liquid that is insoluble with the substance constituting the jet stream, and the jet stream is sequentially formed from a front end in a flow direction at a predetermined rate. It is cut into lengths, and the cut pieces are sequentially formed into seamless capsules or edible particles of a predetermined shape in the liquid flow of the medium liquid, and the seamless capsules or edible particles are collected together with the medium liquid through a collection pipe. In the manufacturing apparatus configured as described above, a sedimentation tank is provided in a state where the medium liquid flows from the collection pipe.

前記沈殿槽は、内部を複数の室に区分し又は複数並設
し、前記回収管からの媒体液が、第一次の室又は沈殿槽
を経て順次第二次以下の室又は沈殿槽へ流れる状態に構
成するのが好ましく、この場合において、媒体液が室又
は沈殿槽から次の室又は沈殿槽へ流れる毎に流れ方向が
上下方向に変わるように、すなわち、上下方向へ蛇行状
に流れるよう構成するのがさらに好ましい。
The sedimentation tank is divided into a plurality of chambers or a plurality of juxtaposed, and the medium liquid from the recovery pipe flows to the second or lower chamber or the sedimentation tank sequentially through the first chamber or the sedimentation tank. In this case, it is preferable that the flow direction changes in the vertical direction each time the medium liquid flows from the chamber or the sedimentation tank to the next chamber or the sedimentation tank, that is, the medium liquid flows in a meandering manner in the vertical direction. It is more preferable to configure.

また、沈殿槽をそれぞれ独立して対に設け、回収管か
らの媒体液が対の沈殿槽のいずれか一方へ選択的に導か
れる状態に構成することができる。
Further, the sedimentation tanks can be independently provided in pairs, so that the medium liquid from the collection pipe can be selectively guided to one of the paired sedimentation tanks.

前記沈殿槽の底部には、バルブ付きの排出口を設ける
のが好ましい。
It is preferable to provide a discharge port with a valve at the bottom of the settling tank.

「作用」 本発明に係る回収装置によると、シームレスカプセル
又は可食粒を含む媒体液は、回収管を経て沈殿槽に流れ
込み、媒体液中のカプセル又は可食粒は沈殿槽内に沈殿
するので、この沈殿後のカプセル又は可食粒を適宜の手
段で取り出して回収する。
According to the recovery device of the present invention, the medium liquid containing the seamless capsules or edible particles flows into the sedimentation tank via the collection pipe, and the capsules or edible particles in the medium liquid precipitate in the sedimentation tank. Then, the capsules or edible grains after the precipitation are taken out and collected by an appropriate means.

第一次の室又は沈殿槽から第二次以下の室又は沈殿槽
へと媒体液が順次流れる状態に構成すると、媒体液の流
速が次第に低下してカプセル又は可食粒の沈殿が促進さ
れる。
When configured so that the medium liquid flows sequentially from the primary chamber or the sedimentation tank to the secondary or lower chamber or the sedimentation tank, the flow rate of the medium liquid gradually decreases, and the sedimentation of capsules or edible particles is promoted. .

沈殿槽をそれぞれ独立して対に設け、回収管からの媒
体液が対の沈殿槽のいずれか一方へ選択的に導かれる状
態に構成すると、粒揃いや造粒状態がよくない時は回収
管からの媒体液を一方の沈殿槽に流し、粒揃いや造粒状
態がよい時は他方の沈殿槽に流すことによって、良品と
不良品を別々に沈殿させ回収することができる。
If the sedimentation tanks are provided independently in pairs, and the medium liquid from the collection tube is selectively guided to either one of the paired sedimentation tanks, if the grain uniformity or granulation state is not good, the sedimentation tanks will be By flowing the medium liquid into one of the sedimentation tanks and flowing the other medium into the sedimentation tank when the grain uniformity and the granulation state are good, good and defective products can be separately precipitated and collected.

沈殿槽の底部にバルブ付きの排出口を設けると、この
排出口を随時開いて当該沈殿槽内の媒体液とともにカプ
セル又は可食粒を取り出すことができる。
If a discharge port with a valve is provided at the bottom of the sedimentation tank, the discharge port can be opened as needed to take out capsules or edible particles together with the medium liquid in the sedimentation tank.

「実施例」 第1図〜第3図を参照して本発明に係る回収装置の実
施例を説明する。
“Embodiment” An embodiment of the recovery apparatus according to the present invention will be described with reference to FIGS. 1 to 3.

なお、回収管に達するまでの製造装置については、前
述のような公知のものを採用することができるのでそれ
らの説明や図示は省略する。
In addition, as for the manufacturing apparatus up to the collection pipe, the known apparatus as described above can be employed, and thus the description and illustration thereof are omitted.

第1図はその一例を示すもので、回収管70の終端部に
は、第1の沈殿槽81及びそれより容積の大きい第2の沈
殿槽82が連続して配置されるとともに、第2の沈殿槽82
の終端に接して補助槽9が設けられ、回収管70からの微
小なシームレスカプセル(又は可食粒)eを含む媒体液
cが、第1の沈殿槽81に流入して第2の沈殿槽82へ流
れ、沈殿槽81,82を流れるときカプセルeが沈殿し、媒
体液cのみがさらに補助槽9ヘ流出するように構成して
いる。
FIG. 1 shows an example of this, in which a first sedimentation tank 81 and a second sedimentation tank 82 having a larger volume than the first sedimentation tank 81 are continuously arranged at the end of the collection pipe 70, and Settling tank 82
An auxiliary tank 9 is provided in contact with the end of the medium, and the medium liquid c containing the minute seamless capsules (or edible particles) e from the collection pipe 70 flows into the first settling tank 81 and the second settling tank 81 The capsule e is settled when flowing into the sedimentation tanks 81 and 82 and only the medium liquid c flows out further to the auxiliary tank 9.

この実施例では、第1の沈殿槽81は底部にまで達しな
い垂直な隔壁板8aによって二つの室811と812とに区分さ
れ、カプセルeを含む媒体液cは、回収管70より第1の
沈殿槽81における第一次の室811へ流入するようになっ
ている。
In this embodiment, the first sedimentation tank 81 is divided into two chambers 811 and 812 by a vertical partition plate 8a that does not reach the bottom. It flows into the first chamber 811 in the settling tank 81.

第一次の室811内に流入した前記媒体液cは一時的に
乱流状態になるが、隔壁8aの下方より流速を低下させつ
つ順次第二次の室812へ流入し、この室812内を上方に向
かって流れる。
The medium liquid c that has flowed into the first chamber 811 is temporarily in a turbulent state, but sequentially flows into the second chamber 812 while lowering the flow velocity from below the partition 8a. Flows upward.

このときの媒体液cの流速はやや早いため、第1の沈
殿槽81内で沈殿するシームレスカプセルeは比較的少な
いが、媒体液cが第2の沈殿槽82との隔壁板8bの上をオ
ーバーフローして第2の沈殿槽82内に流れ込むと、容積
の大きい第2の沈殿槽82内で流速をさらに低下させるの
で、この第2の沈殿槽82内を第1図右方向へ流れると
き、シームレスカプセルeのほとんどが沈殿し、媒体液
cのみが沈殿槽82の終端からオーバーフローして補助槽
9へ流れる。
At this time, the flow rate of the medium liquid c is slightly high, so that the number of the seamless capsules e that settle in the first settling tank 81 is relatively small, but the medium liquid c flows on the partition plate 8b with the second settling tank 82. When overflowing and flowing into the second sedimentation tank 82, the flow rate is further reduced in the second sedimentation tank 82 having a large volume. Therefore, when flowing in the second sedimentation tank 82 to the right in FIG. Most of the seamless capsule e is settled, and only the medium liquid c overflows from the end of the settling tank 82 and flows to the auxiliary tank 9.

補助槽9に溜まった媒体液cは、当該補助槽9の上部
へ連通した媒体液の回収パイプ91を経て、例えば第4図
の回収タンク5へ回収されるように構成する。この回収
パイプ91で回収される媒体液cは、図示しないろ過器を
経て回収タンク5へ回収されるように構成するのが好ま
しい。
The medium liquid c stored in the auxiliary tank 9 is configured to be recovered to, for example, the recovery tank 5 in FIG. 4 through a medium liquid recovery pipe 91 communicating with the upper part of the auxiliary tank 9. It is preferable that the medium liquid c recovered by the recovery pipe 91 be recovered to the recovery tank 5 through a filter (not shown).

沈殿槽81,82の底部には、バルブ86を取付けた排出口8
5がそれぞれ設けられており、製造装置の運転を停止し
たとき、あるいは、沈殿槽81又は82内に沈殿しているカ
プセルeが相当量に達したときは、当該沈殿槽81又は82
の底部のバルブ86を開いて、沈殿しているカプセルeを
当該沈殿槽内の媒体液cとともに取り出し、適当なろ過
手段により媒体液からカプセルを分離する。
At the bottom of the sedimentation tanks 81 and 82, there is an outlet 8 with a valve 86 attached.
5 are provided, respectively, when the operation of the manufacturing apparatus is stopped, or when the amount of the capsule e that has settled in the settling tank 81 or 82 reaches a considerable amount, the settling tank 81 or 82 is set.
The valve 86 at the bottom of is opened to take out the precipitated capsule e together with the medium liquid c in the settling tank, and separate the capsule from the medium liquid by a suitable filtration means.

符号7aは、回収管70の終端からカプルを含む媒体液が
流出するときに、当該媒体液が断続しないで連続して流
出するように、回収管70の終端部分の最上レベル位置に
設けたエアー取入れ口である。
Reference numeral 7a denotes an air provided at the highest level position of the end portion of the collection pipe 70 so that when the medium liquid including the couple flows out from the end of the collection pipe 70, the medium liquid continuously flows out without interruption. It is an intake.

前記実施例の回収装置は、カプセルeがやや軟らかい
状態であっても回収次にカプセルを傷付けることがほと
んどなく、また、網を使用したものでないために、微小
カプセルを回収する際にも目詰まり等の心配がない。
Even if the capsule e is slightly soft, the collecting apparatus of the above embodiment hardly damages the capsule next to the collection, and since the mesh is not used, clogging also occurs when collecting the microcapsules. There is no need to worry.

第2図は他の実施例を示すもので、対の沈殿槽83,84
を設置し、沈殿槽83,84の中間の上方へ回収管70の終端
を下向きに臨ませ、その真下に案内板80を所定角度範囲
で回動する状態に設け、この案内板80を、一方の沈殿槽
83の方へ先下がり状になるように回動させるか、又は他
方の沈殿槽84の方へ先下がり状になるように回動させる
ことにより、回収管70から流出するカプセルeを含む媒
体液cをいずれか一方の沈殿槽83又は84へ選択的に流入
させ得る状態に構成している。
FIG. 2 shows another embodiment, in which a pair of settling tanks 83 and 84 are provided.
Is installed, with the end of the recovery pipe 70 facing downward above the middle of the sedimentation tanks 83 and 84, and a guide plate 80 is provided directly below the guide tube 80 so as to rotate within a predetermined angle range. Settling tank
The medium liquid containing the capsule e flowing out of the collection pipe 70 is rotated by turning so as to fall down toward 83 or by turning so as to fall down toward the other settling tank 84. It is configured such that c can selectively flow into one of the settling tanks 83 or 84.

この実施例の回収装置において、媒体液cは、一方の
沈殿槽83では同図左端より右方に流れ、他方沈殿槽84で
は同図右端より左方に流れるようになっており、それぞ
れ流れ方向終端の上部に回収パイプ91が連通されてい
る。
In the recovery apparatus of this embodiment, the medium liquid c flows rightward from the left end in the figure in one sedimentation tank 83, and flows leftward from the right end in the figure in the sedimentation tank 84. A recovery pipe 91 communicates with the upper end of the terminal.

沈殿槽83(84)は、媒体液cの流れ方向へ先上がり状
に傾斜した隔壁案8c,8d,8eによって、第一次の室831(8
41),第二次の室832(842),第三次の室833(843),
第四次の室834(844)とにそれぞれ区分されており、隔
壁板8cと隔壁板8eは沈殿槽83(84)の内底面から浮上し
て上端に達し、中間の隔壁板8dはその下端を沈殿槽83
(84)の内底面に接触させるとともに、その上端を媒体
液cの最上面レベル以下に設定している。
The sedimentation tank 83 (84) is divided into first chambers 831 (8) by partition walls 8c, 8d, and 8e that are inclined upward in the flow direction of the medium liquid c.
41), second room 832 (842), third room 833 (843),
The partition wall 8c and the partition plate 8e float up from the inner bottom surface of the sedimentation tank 83 (84) to reach the upper end, and the middle partition plate 8d is divided into the fourth lower chamber 834 (844). The sedimentation tank 83
(84), and the upper end thereof is set to be lower than the uppermost level of the medium liquid c.

したがって、沈殿槽83(84)内において、回収管70か
ら流出するカプセルeを含む媒体液cは、第一次の室83
1(841)から第四次の室834(844)へと上下方向へ蛇行
するように流れながら流速を低下させ、次第に遅くなる
流れの過程でカプセルeの沈殿が促進される。
Therefore, in the settling tank 83 (84), the medium liquid c containing the capsule e flowing out of the recovery pipe 70 is supplied to the first chamber 83.
The flow velocity is reduced while flowing in a meandering manner from 1 (841) to the fourth chamber 834 (844), and the sedimentation of the capsule e is promoted in the course of the gradually decreasing flow.

カプセルeが沈殿した後の媒体液cは、回収パイプ91
を経て例えば第4図における媒体液の回収タンク5に回
収される。
The medium liquid c after the capsule e has settled is collected in the recovery pipe 91.
After that, the medium is collected in the medium tank 5 shown in FIG. 4, for example.

この実施例においても、沈殿槽83,84の底部の所要の
部分には、バルブ86を取付けた排出口85がそれぞれ設け
られており、沈殿したカプセルeは、沈殿槽83,84内に
溜まっている媒体液cとともに適宜排出口85から取り出
せるようになっている。
Also in this embodiment, a discharge port 85 to which a valve 86 is attached is provided at a required portion at the bottom of the sedimentation tanks 83 and 84, and the precipitated capsule e is accumulated in the sedimentation tanks 83 and 84. It can be appropriately taken out from the discharge port 85 together with the medium liquid c.

例えば、シームレスカプセル又は可食粒の製造装置に
おいて、運転開始当初は粒揃いその他粒の形成状態がわ
るく、運転中にも形成状態がわるくなることがあり得る
が、この実施例では、前述のように対の沈殿槽83,84を
設け、回収管70からの媒体液cをいずれか一方の沈殿槽
83又は84へ選択的に流れ得るように構成しているので、
粒揃いその他粒の形成状態の悪化を検出したときは、一
方の沈殿槽83から他方の沈殿槽84へと媒体液cの流れを
変えることにより、良品と不良品とを分けて回収するこ
とができる。
For example, in a manufacturing device for seamless capsules or edible grains, the formation state of uniform grains and other grains may be poor at the beginning of the operation, and the formation state may be poor during the operation, but in this embodiment, as described above, A pair of sedimentation tanks 83 and 84 are provided, and the medium liquid c from the collection pipe 70 is set in one of the sedimentation tanks.
Because it is configured to selectively flow to 83 or 84,
When it is detected that the uniformity of the grains and the deterioration of the grain formation state are detected, by changing the flow of the medium liquid c from one sedimentation tank 83 to the other sedimentation tank 84, non-defective products and defective products can be separately collected. .

第2図の実施例において、隔壁板8c,8d,8eは垂直に設
けてもよく、また、案内板80はこれに代えて回収管70の
先端に図示しないフレキシブルな短い管を連結し、当該
フレキシブルな管を沈殿槽83又は84へ選択的に向け得る
ように構成しても、あるいは回収管70の先端にL字状の
管を回動するように連結し、当該L字状の管を沈殿槽83
又は84へ選択的に向け得るように構成しても実施するこ
とができる。
In the embodiment shown in FIG. 2, the partition plates 8c, 8d and 8e may be provided vertically, and the guide plate 80 is connected to a flexible short pipe (not shown) at the tip of the collection pipe 70 instead. Even if a flexible tube can be selectively directed to the sedimentation tank 83 or 84, or an L-shaped tube is pivotally connected to the tip of the collection tube 70, and the L-shaped tube is Settling tank 83
Alternatively, the present invention can also be implemented by a configuration that can be selectively directed to 84.

第2図の実施例の装置における他の構成や作用は、第
1図の実施例の装置におけるものと同様なのでそれらの
説明は省略する。
Other configurations and operations of the apparatus of the embodiment shown in FIG. 2 are the same as those of the apparatus of the embodiment shown in FIG. 1, and the description thereof will be omitted.

前記各実施例では、沈殿槽81(82、83、84)の底部へ
排出口85を設け、この排出口85を開けて沈殿したカプセ
ルを溜まっている媒体液とともに取り出すようにした
が、カプセルの粒径や固さによっては沈殿したものをす
くって取り出すことができるし、粒径の比較的大きいカ
プセルを回収する場合においては、第3図のように、沈
殿槽87内に網又は多孔板からなるバスケット88を設け、
回収管70から沈殿槽87内に媒体液cとともに流入するカ
プセルeを、前記バスケット88内に沈殿させ、このバス
ケット88を沈殿槽87から適宜取り出すように構成しても
実施することができる。
In each of the above embodiments, the outlet 85 is provided at the bottom of the settling tank 81 (82, 83, 84), and the outlet 85 is opened to take out the precipitated capsule together with the accumulated medium liquid. Depending on the particle size and hardness, the precipitate can be scooped and taken out. When collecting capsules having a relatively large particle size, as shown in FIG. A basket 88
The capsule e flowing from the collection pipe 70 into the sedimentation tank 87 together with the medium liquid c is settled in the basket 88, and the basket 88 can be appropriately removed from the sedimentation tank 87.

なお、本発明に係る回収装置は前記実施例のみに限定
されず、特許請求の範囲内において、適宜変更しあるい
は他の部材を付加して実施することができる。
In addition, the recovery apparatus according to the present invention is not limited to the above-described embodiment, and can be implemented by appropriately changing or adding other members within the scope of the claims.

「発明の効果」 本発明に係るシームレスカプセル又は可食粒の回収装
置は、対象物を媒体液とともに回収管から沈殿槽に流入
させ、沈殿槽で沈殿させてから回収することができるか
ら、従来のように、固い網に向けて媒体液とともに落下
させるのもと異なり、カプセル又は可食粒の表面が軟ら
かい場合でもその表面を傷付けることがほとんどなく、
また、カプセル又は可食粒が微小な場合でも目詰まりの
問題を生じない。
[Effect of the Invention] The seamless capsule or edible particle collection device according to the present invention can flow an object together with a medium liquid from a collection tube into a sedimentation tank, and settle it in the sedimentation tank and then recover it. Unlike the case where the surface of the capsule or edible grains is soft, unlike the case of dropping with a medium liquid toward a hard net, there is almost no damage to the surface,
In addition, even if the capsules or edible particles are minute, the problem of clogging does not occur.

【図面の簡単な説明】[Brief description of the drawings]

第1図は本発明に係る回収装置の一例を示す断面図、第
2図及び第3図は、それぞれ回収装置の他の実施例を示
す断面図、第4図は、従来のシームレスカプセルの回収
装置を含む製造装置を、一部を断面にして示した配管図
である。 図中主要符号の説明 cは媒体液、dはジェット流、eはシームレスカプセ
ル、5は媒体液の回収タンク、70は回収管、80は案内
板、81,82,83,84,87は沈殿槽、8a,8b,8c,8d,8eは隔壁
板、811,831,841は第一次の室、812,832,842は第二次の
室、833,843は第三次の室、834,844は第四次の室、85は
排出口、86はバルブ、9は補助槽、91は回収パイプであ
る。
FIG. 1 is a cross-sectional view showing an example of the recovery apparatus according to the present invention, FIGS. 2 and 3 are cross-sectional views showing another embodiment of the recovery apparatus, respectively, and FIG. FIG. 3 is a piping diagram showing a part of the manufacturing apparatus including the apparatus in cross section. Explanation of main symbols in the figure c is a medium liquid, d is a jet flow, e is a seamless capsule, 5 is a medium liquid recovery tank, 70 is a recovery pipe, 80 is a guide plate, 81, 82, 83, 84, 87 is sedimentation Tanks, 8a, 8b, 8c, 8d, 8e are partition plates, 811,831,841 is the first room, 812,832,842 is the second room, 833,843 is the third room, 834,844 is the fourth room, and 85 is the drain. The outlet, 86 is a valve, 9 is an auxiliary tank, and 91 is a recovery pipe.

フロントページの続き (72)発明者 細井 富也 東京都豊島区高田3丁目24番1号 大正 製薬株式会社内 (72)発明者 生田 賢一 東京都豊島区高田3丁目24番1号 大正 製薬株式会社内 (56)参考文献 特開 昭61−151119(JP,A) (58)調査した分野(Int.Cl.6,DB名) B01J 13/02 - 13/22 A61K 9/00 - 9/72 A23L 1/00 - 1/035 A23P 1/00 - 1/16 B01J 2/00 - 2/30Continuing on the front page (72) Inventor Tomoya Hosoi 3- 24-1, Takada, Toshima-ku, Tokyo Inside Taisho Pharmaceutical Co., Ltd. (72) Inventor Kenichi Ikuta 3-24-1, Takada, Toshima-ku, Tokyo Taisho Pharmaceutical Co., Ltd. (56) References JP-A-61-151119 (JP, A) (58) Fields investigated (Int. Cl. 6 , DB name) B01J 13/02-13/22 A61K 9/00-9/72 A23L 1/00-1/035 A23P 1/00-1/16 B01J 2/00-2/30

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】粘性及び流動性を有する物質の流れからな
るジェット流を、当該ジェット流を構成する物質とは非
溶解な媒体液の液流中で連続的に形成し、当該ジェット
流を流れ方向先端より順次所定長さに切断し、切断した
ものを前記媒体液の液流中で順次所定形状のシームレス
カプセル又は可食粒に形成し、このシームレスカプセル
又は可食粒を前記媒体液とともに回収管を経て回収すべ
く構成した製造装置において、前記回収管から媒体液が
流入する状態に沈殿槽を設けたことを特徴とする、シー
ムレスカプセル又は可食粒の回収装置。
1. A jet stream comprising a flow of a substance having viscosity and fluidity is continuously formed in a stream of a medium liquid insoluble in a substance constituting said jet stream. Cut into a predetermined length sequentially from the front end in the direction, and the cut pieces are sequentially formed into seamless capsules or edible particles of a predetermined shape in the liquid flow of the medium liquid, and the seamless capsules or edible particles are collected together with the medium liquid. A manufacturing apparatus configured to recover via a pipe, wherein a settling tank is provided in a state where the medium liquid flows in from the recovery pipe, wherein the apparatus for recovering seamless capsules or edible particles is provided.
【請求項2】沈殿槽内を複数の室に区分し又は沈殿槽を
複数並設し、前記回収管からの媒体液が、第一次の室又
は沈殿槽を経て順次第二次以下の室又は沈殿槽へ流れる
状態に構成したことを特徴とする、請求項1に記載のシ
ームレスカプセル又は可食粒の回収装置。
2. The sedimentation tank is divided into a plurality of chambers or a plurality of sedimentation tanks are juxtaposed, and the medium liquid from the recovery pipe is sequentially passed through the first chamber or the sedimentation tank to the second and lower chambers. The seamless capsule or edible particle collecting device according to claim 1, wherein the device is configured to flow into a sedimentation tank.
【請求項3】沈殿槽をそれぞれ独立して対に設け、回収
管からの媒体液が対の沈殿槽のいずれか一方へ選択的に
導かれる状態に構成したことを特徴とする、請求項1に
記載のシームレスカプセル又は可食粒の回収装置。
3. A sedimentation tank is provided in each of the pairs independently, so that the medium liquid from the collection tube is selectively guided to one of the paired sedimentation tanks. 2. A device for collecting seamless capsules or edible particles according to 1.
【請求項4】沈殿槽の底部にバルブ付きの排出口を設け
た、請求項1又は2若しくは3に記載のシームレスカプ
セル又は可食粒の回収装置。
4. The seamless capsule or edible particle recovery device according to claim 1, wherein a discharge port with a valve is provided at the bottom of the sedimentation tank.
JP1254623A 1989-09-29 1989-09-29 Collection device for seamless capsules or edible grains Expired - Lifetime JP2801682B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1254623A JP2801682B2 (en) 1989-09-29 1989-09-29 Collection device for seamless capsules or edible grains

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1254623A JP2801682B2 (en) 1989-09-29 1989-09-29 Collection device for seamless capsules or edible grains

Publications (2)

Publication Number Publication Date
JPH03114529A JPH03114529A (en) 1991-05-15
JP2801682B2 true JP2801682B2 (en) 1998-09-21

Family

ID=17267602

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1254623A Expired - Lifetime JP2801682B2 (en) 1989-09-29 1989-09-29 Collection device for seamless capsules or edible grains

Country Status (1)

Country Link
JP (1) JP2801682B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101874618B1 (en) * 2018-02-27 2018-07-05 정수영 Device for manufacturing a soft-round gel

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101874618B1 (en) * 2018-02-27 2018-07-05 정수영 Device for manufacturing a soft-round gel

Also Published As

Publication number Publication date
JPH03114529A (en) 1991-05-15

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